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Characteristic function reaction

Reaction of Enolate Anions. In the presence of certain bases, eg, sodium alkoxide, an ester having a hydrogen on the a-carbon atom undergoes a wide variety of characteristic enolate reactions. Mechanistically, the base removes a proton from the a-carbon, giving an enolate that then can react with an electrophile. Depending on the final product, the base may be consumed stoichiometricaHy or may function as a catalyst. Eor example, the sodium alkoxide used in the Claisen condensation is a catalyst ... [Pg.389]

Each functional group of an amino acid exhibits all of its characteristic chemical reactions. For carboxylic acid groups, these reactions include the formation of esters, amides, and acid anhydrides for amino groups, acylation, amidation, and esterification and for —OH and —SH groups, oxidation and esterification. The most important reaction of amino acids is the formation of a peptide bond (shaded blue). [Pg.18]

Fig. 4. Variation of autocorrelation function with changes in the equilibrium constant in the fast reaction limit. A and B have the same diffusion coefficients but different optical (fluorescence) properties. A difference in the fluorescence of A and B serves to indicate the progress of the isomerization reaction the diffusion coefficients of A and B are the same. The characteristic chemical reaction time is in the range of 10 4-10-5 s, depending on the value of the chemical relaxation rate that for diffusion is 0.025 s. For this calculation parameter values are the same as those for Figure 3 except that DA = Z)B = lO"7 cm2 s-1 and QA = 0.1 and <9B = 1.0. The relation of CB/C0 to the different curves is as in Figure 3. [Pg.121]

The reaction will then appear to follow first-order kinetics, regardless of the functional form of the intrinsic rate expression and of the effectiveness factor. This first-order dependence is characteristic of reactions that are mass transfer limited. The term diffusion controlled is often applied to reactions that occur under these conditions. [Pg.478]

The transformation of the chain end active center from one type to another is usually achieved through the successful and efficient end-functionalization reaction of the polymer chain. This end-functionalized polymer can be considered as a macroinitiator capable of initiating the polymerization of another monomer by a different synthetic method. Using a semitelechelic macroinitiator an AB block copolymer is obtained, while with a telechelic macroinitiator an ABA triblock copolymer is provided. The key step of this methodology relies on the success of the transformation reaction. The functionalization process must be 100% efficient, since the presence of unfunctionalized chains leads to a mixture of the desired block copolymer and the unfunctionalized homopolymer. In such a case, control over the molecular characteristics cannot be obtained and an additional purification step is needed. [Pg.62]

The first term is the double-layer charging response, while the second is a measure of the overlap between double-layer charging and Faradaic reaction, which eventually tends toward the Faradaic response that would have been obtained if double-layer charging were absent. As to the expression of the characteristic functions f(s) and f(t) in the Laplace and original spaces, respectively, with the same notations as in Section 6.1.4,... [Pg.363]

The previous chapter offered a broad overview of peptidases and esterases in terms of their classification, localization, and some physiological roles. Mention was made of the classification of hydrolases based on a characteristic functionality in their catalytic site, namely serine hydrolases, cysteine hydrolases, aspartic hydrolases, and metallopeptidases. What was left for the present chapter, however, is a detailed presentation of their catalytic site and mechanisms. As such, this chapter serves as a logical link between the preceding overview and the following chapters, whose focus is on metabolic reactions. [Pg.65]

While in most of the reports on SIP free radical polymerization is utihzed, the restricted synthetic possibihties and lack of control of the polymerization in terms of the achievable variation of the polymer brush architecture limited its use. The alternatives for the preparation of weU-defined brush systems were hving ionic polymerizations. Recently, controlled radical polymerization techniques has been developed and almost immediately apphed in SIP to prepare stracturally weU-de-fined brush systems. This includes living radical polymerization using nitroxide species such as 2,2,6,6-tetramethyl-4-piperidin-l-oxyl (TEMPO) [285], reversible addition fragmentation chain transfer (RAFT) polymerization mainly utilizing dithio-carbamates as iniferters (iniferter describes a molecule that functions as an initiator, chain transfer agent and terminator during polymerization) [286], as well as atom transfer radical polymerization (ATRP) were the free radical is formed by a reversible reduction-oxidation process of added metal complexes [287]. All techniques rely on the principle to drastically reduce the number of free radicals by the formation of a dormant species in equilibrium to an active free radical. By this the characteristic side reactions of free radicals are effectively suppressed. [Pg.423]

The flame lift-off height, which is related to the ignition distance, was inversely affected by the excitation frequency. Since the flow time scale decreased with increasing frequency, the data were plotted as a function of the Damkohler number in Fig. 29.14, where the characteristic flow time scale was estimated by large-eddy turnover time as 1/17 and the characteristic chemical reaction time was computed using an ignition delay model [21] for ethylene jet. While the results did not show any evidence of critical Damkohler number, the range... [Pg.482]

Figures 6.1-6.3 present the curves of consumption of SnBu4 as a function of time for Pt, Ni and Cu catalysts. Pt (Figure 6.1) and Ni-based (Figure 6.2) systems have similar characteristics. The reaction rate presents two well-differentiated stages a faster one, during the first 30 min of reaction, and a slower one, which reaches a defined plateau. For Cu (Figure 6.3), the results do not show these two weU-differentiated stages. Figures 6.1-6.3 present the curves of consumption of SnBu4 as a function of time for Pt, Ni and Cu catalysts. Pt (Figure 6.1) and Ni-based (Figure 6.2) systems have similar characteristics. The reaction rate presents two well-differentiated stages a faster one, during the first 30 min of reaction, and a slower one, which reaches a defined plateau. For Cu (Figure 6.3), the results do not show these two weU-differentiated stages.
The fundamental question in transport theory is Can one describe processes in nonequilibrium systems with the help of (local) thermodynamic functions of state (thermodynamic variables) This question can only be checked experimentally. On an atomic level, statistical mechanics is the appropriate theory. Since the entropy, 5, is the characteristic function for the formulation of equilibria (in a closed system), the deviation, SS, from the equilibrium value, S0, is the function which we need to use for the description of non-equilibria. Since we are interested in processes (i.e., changes in a system over time), the entropy production rate a = SS is the relevant function in irreversible thermodynamics. Irreversible processes involve linear reactions (rates 55) as well as nonlinear ones. We will be mainly concerned with processes that occur near equilibrium and so we can linearize the kinetic equations. The early development of this theory was mainly due to the Norwegian Lars Onsager. Let us regard the entropy S(a,/3,. ..) as a function of the (extensive) state variables a,/ ,. .. .which are either constant (fi,.. .) or can be controlled and measured (a). In terms of the entropy production rate, we have (9a/0f=a)... [Pg.63]

The chemistry behind the detonation of organic compounds is exceedingly complex and poorly understood, because it involves a variety of intermolecular reactions different from those observed during thermolysis in solution or in the gas phase [92-94], The conditions required to induce detonation of organic explosives vary widely and no clear-cut structure-sensitivity relationship exists. Nevertheless, most known explosives contain characteristic functional groups, and small molecules containing several of these should be handled with great care. [Pg.52]

Fig. 7. The characteristic functions of rj vs. Fig. 7. The characteristic functions of rj vs. <p, determining activity of porous catalyst due to diffusion effects. A cylindrical channel, first-order reaction B spherical particle, first-order reaction C cylindrical channel, second-order reactions.
Effect of reaction order on diffusion factor y. Calculation of the characteristic function of y applicable to the case of an n order reaction yields similar functional relationships, in which the modulus

concentration term. For example, the case of second-order reaction involves the modulus... [Pg.161]

Fig. 8. The characteristic function of i vs. Fig. 8. The characteristic function of i vs. <phi, determining activity of porous catalyst in terms of observable variables lumped into the modulus (Sphere, first-order reaction.)...
It was recognized early on that the functional isocyano group differs profoundly from any other functional class of chemical compounds. In the 1890s, Nef [44] had mentioned the fact that the functional group -NC of the isocyanides contains a divalent carbon atom C11, and therefore their chemistry differs very much from other stable organic chemical compounds that contain only tetravalent carbon atoms CIV. Any synthesis of the isocyanides corresponds to a conversion of Clv into C",and all characteristic chemical reactions of the isocyanides correspond to exothermic irreversible transitions of the carbon atoms C11 into CIV. Under the correct conditions, when no competing formation of by-products takes place, such reactions yield the products quantitatively. [Pg.131]


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